Apparatus for manufacturing an optical fiber

ABSTRACT

An apparatus for manufacturing an optical fiber including: a drawing portion; a coating portion; and a curing portion, wherein: a direction changer which changes a direction of the bare optical fiber is disposed in any position from the drawing portion to the coating portion; the direction changer includes a guide groove which guides the bare optical fiber; a blowout port of a fluid which floats the bare optical fiber wired along the guide groove is formed along the guide groove in the guide groove; and in the blowout port, the Reynolds number in an inlet wire portion of the bare optical fiber to the guide groove and an outlet wire portion from the guide groove is greater than the Reynolds number in an intermediate portion between the inlet wire portion and the outlet wire portion.

CROSS REFERENCE TO RELATED APPLICATIONS

This application is a Divisional of U.S. application Ser. No 14/757,428,filed on Dec. 23, 2015, claiming priority from Japanese PatentApplication No. 2014-266308, filed on Dec. 26, 2014, the entire contentsof which are incorporated herein by reference.

BACKGROUND OF THE INVENTION

Field of the Invention

The present invention relates to an apparatus for manufacturing anoptical fiber.

Description of Related Art

FIG. 15 is a schematic view showing a schematic configuration of anexample of an apparatus of manufacturing an optical fiber of the relatedart.

The manufacturing apparatus includes a drawing unit 10 which forms abare optical fiber 3 from an optical fiber preform 2, a cooling unit 120which cools the bare optical fiber 3, a coating unit 30 which disposes acoating layer on the bare optical fiber 3 and forms an optical fiberintermediary body 4, and a curing unit 40 which cures the coating layerof the optical fiber intermediary body 4 to be an optical fiber 5.

During manufacturing the bare optical fiber, the bare optical fiber 3 isobtained by drawing the optical fiber preform 2 at the drawing portion10. After cooling the bare optical fiber 3 at the cooling portion 120, acoating layer made of a resin is provided at an outer surface of thebare optical fiber 3 at the coating portion 30. The bare optical fiber 3in which the coating layer is cured at the curing unit 40 is wound bywinding means 70 through a pulley 50 and a take-up unit 60.

The bare optical fiber 3 obtained by drawing the optical fiber preform 2is drawn toward a vertically lower direction along a linear path.

In the manufacturing method, there is a restriction on the height of theentire system as a factor affecting productivity. The reason that theheight of the system is a main factor which restricts productivity isbecause it is necessary to ensure a distance for sufficiently cooling abare optical fiber which is obtained by drawing the optical fiberpreform.

When a new facility including a building is built, the restriction canbe relaxed; however, an enormous cost is required for building a newfacility, and when it is required that productivity is further improvedin the future, it is necessary that a new facility will be built athigher cost.

As a method of relaxing the restriction, a method is included in which adirection changer including a non-contact retaining mechanism is used.

The non-contact retaining mechanism is for holding a target to be in anoncontact state using the pressure of a fluid such as air, and in thedirection changer including the fluid bearing, it is possible to performdirection change with respect to the bare optical fiber without being incontact with the bare optical fiber (a bare fiber).

By using the direction changer, it is possible to change the directionof the bare optical fiber which is subjected to the fiber drawing fromthe optical fiber preform along the first path to conform to a secondpath (for example, refer to Japanese Patent No. 5571958 and JapaneseUnexamined Patent Application, First Publication No. S62-003037).

In Japanese Patent No. 5571958, a manufacturing method is disclosed inwhich an apparatus for direction change including a groove into which anoptical fiber is introduced and an opening formed in the groove is used.In this method, gas introduced to the apparatus is blown out from theopening through one inflow port, and the direction of the optical fiberis changed in a state where the optical fiber is floated due to thepressure of the gas.

A direction changer disclosed in Japanese Unexamined Patent Application,First Publication No. S62-003037 includes a guide groove which guides abare optical fiber, and a blowout port for gas which is formed on alower surface and both side surfaces of the guide groove (refer toExamples, and FIGS. 3A to 4). In the manufacturing method using thedirection changer, the direction of the optical fiber is changed in astate where the optical fiber is floated due to the pressure of the gasblown out from four blowout ports.

However, in the manufacturing method described in the above-describedJapanese Unexamined Patent Application, it is not easy to stably floatthe bare optical fiber in a tool for the direction changer.

The present invention has been made in consideration of theabove-described circumstances and to provide a method of manufacturingan optical fiber and an apparatus of manufacturing an optical fibercapable of stably floating the bare optical fiber.

SUMMARY OF THE INVENTION

A first aspect of the present invention is a method of manufacturing anoptical fiber including, drawing an optical fiber preform and forming abare optical fiber; disposing a coating layer formed of a resin on theouter circumference of the bare optical fiber; and curing the coatinglayer and obtaining an optical fiber. A direction of the bare opticalfiber is changed by a direction changer in any position from drawing theoptical fiber to disposing the coating layer, the direction changerincludes a guide groove which guides the bare optical fiber, a blowoutport of a fluid which floats the bare optical fiber wired along theguide groove is formed along the guide groove in the guide groove, whena direction of the bare optical fiber is changed by the directionchanger, the fluid is introduced into the guide groove from the blowoutport and the bare optical fiber is floated and a Reynolds number of thefluid is in a range of 1200-3500, and the Reynolds number in an inletwire portion of the bare optical fiber to the guide groove and an outletwire portion from the guide groove is greater than the Reynolds numberin an intermediate portion between the inlet wire portion and the outletwire portion.

In a second aspect of the present invention according to the method ofmanufacturing an optical fiber of the first aspect described above, theReynolds number is controlled by measuring a flotation amount of thebare optical fiber is measured and adjusting an introduced flow volumeof the fluid to the direction changer based on a measurement value ofthe flotation amount.

In a third aspect of the present invention according to the method ofmanufacturing an optical fiber of the first aspect or the second aspectdescribed above, the Reynolds number is adjusted such that a width ofthe blowout ports in the inlet wire portion and the outlet wire portionis set to be smaller than the blowout port in the intermediate portion.

In a fourth aspect of the present invention according to the method ofmanufacturing an optical fiber of the first aspect or the second aspectdescribed above, an internal space for transferring the fluid to theblowout port is ensured inside the direction changer, the internal spacehas a first space which is in communication with the blowout ports inthe inlet wire portion and the outlet wire portion and a second spacewhich is in communication with the blowout port in the intermediateportion, and by adjusting an supply of the fluid to the first space andthe second space, the Reynolds number of the fluid in the inlet wireportion and the outlet wire portion is set to be greater than theReynolds number of the fluid in the intermediate portion.

In a fifth aspect of the present invention according to the method ofmanufacturing an optical fiber of the first aspect or the second aspectdescribed above, an internal space for transferring the fluid to theblowout port is ensured inside the direction changer, the internal spacehas a first space which is in communication with the blowout port in theinlet wire portion, a second space which is in communication with theblowout port in the intermediate portion, and a third space which is incommunication with the blowout port in the outlet wire portion, and byadjusting an supply of the fluid at the first space to the third space,the Reynolds number of the fluid in the inlet wire portion and theoutlet wire portion is set to be greater than the Reynolds number of thefluid in the intermediate portion.

In a sixth aspect of the present invention according to the method ofmanufacturing an optical fiber of the first aspect or the second aspectdescribed above, a narrow portion which is in communication with theblowout ports in the inlet wire portion and the outlet wire portion isformed inside the direction changer, and a pressure loss at the time ofblowing out the fluid in the inlet wire portion and the outlet wireportion is greater than the pressure loss in the intermediate portion,thereby, the Reynolds number of the fluid in the inlet wire portion andthe outlet wire portion is set to be greater than the Reynolds number ofthe fluid in the intermediate portion.

A seventh aspect of the present invention is an apparatus ofmanufacturing an optical fiber including a drawing portion configured todraw an optical fiber perform and form a bare optical fiber, a coatingportion configured to dispose a coating layer formed of a resin on anouter circumference of the bare optical fiber, ad a curing portionconfigured to cure the coating layer. A direction changer which changesa direction of the bare optical fiber is disposed in any position fromthe drawing portion to the coating portion, the direction changerincludes a guide groove which guides the bare optical fiber, a blowoutport of a fluid which floats the bare optical fiber wired along theguide groove is formed along the guide groove in the guide groove, andin the blowout port, the Reynolds number in an inlet wire portion of thebare optical fiber to the guide groove and an outlet wire portion fromthe guide groove is greater than the Reynolds number in an intermediateportion between the inlet wire portion and the outlet wire portion.

In an eighth aspect of the present invention according to the apparatusof manufacturing an optical fiber of the seventh aspect described above,the Reynolds number of the fluid in the inlet wire portion and theoutlet wire portion can be set to be greater than the Reynolds number ofthe fluid in the intermediate portion such that a width of the blowoutports in the inlet wire portion and the outlet wire portion is set to besmaller than the blowout port in the intermediate portion.

In an ninth aspect of the present invention according to the apparatusof manufacturing an optical fiber of the seventh aspect described above,an inner space portion which transports the fluid to the blowout port isensured inside the direction changer, and the inner space portion caninclude a first space portion which is in communication with the blowoutport of the inlet wire portion and the outlet wire portion, and a secondspace portion which is in communication with the blowout port of theintermediate portion.

In a tenth aspect of the present invention according to the apparatus ofmanufacturing an optical fiber of the seventh aspect described above, aninner space portion which transports the fluid to the blowout port isensured inside the direction changer, and the inner space portion caninclude a first space portion which is in communication with the blowoutport of the inlet wire portion, a second space portion which is incommunication with the blowout port of the intermediate portion, and athird space portion which is in communication with the blowout port ofthe outlet wire portion.

In a eleventh aspect of the present invention according to the apparatusof manufacturing an optical fiber of the seventh aspect described above,a narrow portion which is in communication with the blowout ports in theinlet wire portion and the outlet wire portion is formed inside thedirection changer, and a pressure loss at the time of blowing out thefluid in the inlet wire portion and the outlet wire portion is greaterthan the pressure loss in the intermediate portion, thereby, theReynolds number of the fluid in the inlet wire portion and the outletwire portion is set to be greater than the Reynolds number of the fluidin the intermediate portion.

According to the aspects of the present invention described above, whenthe fluid is introduced into the guide groove from the blowout port ofthe direction changer to float the bare optical fiber, a Reynolds numberof the fluid is in a range of 1200-3500, thereby, it is possible tostably float the bare optical fiber.

BRIEF DESCRIPTION OF THE DRAWINGS

FIG. 1 is a schematic view showing a schematic configuration of a firstembodiment of an apparatus of manufacturing an optical fiber.

FIG. 2 is a schematic view showing a sectional structure of a directionchanger of the manufacturing apparatus shown in FIG. 1.

FIG. 3A is a front view showing a first example of the directionchanger.

FIG. 3B is a development view showing a blowout port of the directionchanger shown in FIG. 3A.

FIG. 4 is a front view showing a modification example of the directionchanger of the first example shown in FIGS. 3A and 3B.

FIG. 5A is a front view showing a second example of the directionchanger.

FIG. 5B is a development view showing a blowout port of the directionchanger shown in FIG. 5A.

FIG. 6 is a front view showing a modification example of the directionchanger of the first example shown in FIGS. 5A and 5B.

FIG. 7 is a diagram showing an example of fluctuation of a flotationposition.

FIG. 8 is a diagram showing a Reynolds-number distribution in acircumferential direction of the direction changer of the first example.

FIG. 9 is a diagram showing a Reynolds-number distribution in acircumferential direction of the direction changer of the secondexample.

FIG. 10 is a front view showing a third example of the directionchanger.

FIG. 11 is a front view showing a fourth example of the directionchanger.

FIG. 12 is a front view showing a fifth example of the directionchanger.

FIG. 13A is a schematic view showing a sectional structure of thedirection changer taken along line I-I shown in FIG. 12.

FIG. 13B is a schematic view showing a sectional structure of thedirection changer taken along line II-II shown in FIG. 12.

FIG. 14 is a schematic view showing a schematic configuration of asecond embodiment of an apparatus of manufacturing an optical fiberaccording to the present invention.

FIG. 15 is a schematic view showing a schematic configuration of anexample of an apparatus of manufacturing an optical fiber of the relatedart.

DETAILED DESCRIPTION OF THE INVENTION

FIG. 1 is a schematic view showing a schematic configuration of amanufacturing apparatus 1A which is a first embodiment of an apparatusof manufacturing an optical fiber according to the present invention.

The manufacturing apparatus 1A includes a drawing unit 10, directionchangers 20 (20A and 20B), a position sensor 80, a coating unit 30, acuring unit 40, and a control unit 90.

A reference numeral “2 a” is a tip end portion of a diameter reducedportion (neck-down) of the optical fiber preform 2 which is heated andmelted.

The drawing unit 10 includes a heating furnace 11, and forms the bareoptical fiber 3 by heating the optical fiber preform 2 using a heatingfurnace 11 and by drawing the optical fiber preform 2.

The direction changers 20 (20A and 20B) change the direction of the bareoptical fiber 3. In the manufacturing apparatus 1A, two directionchangers 20 are used. The respective direction changers 20 are referredto as the first direction changer 20A and the second direction changer20B from upstream to downstream in a drawing direction.

The first direction changer 20A among the two direction changers 20changes the direction of the bare optical fiber 3 which is drawn out toa vertically downward direction from the optical fiber preform 2 to ahorizontal direction, and the second direction changer 20B changes thedirection of the bare optical fiber 3 to the vertically downwarddirection.

The coating unit 30 applies (coats) a coating material such as aurethane acrylate-based resin onto the outer circumference of the bareoptical fiber 3 to be the coating layer, and thus obtains the opticalfiber intermediary body 4.

The resin coating, for example, is two-layer coating in which a materialfor a primary coating layer having a low Young's modulus is applied tothe inside, and a material for a secondary coating layer having a highYoung's modulus is applied to the outside. The used material, forexample, is an ultraviolet curing resin.

The coating unit 30 may have a configuration in which the primarycoating layer and the secondary coating layer are separately coated, ormay have a configuration in which the primary coating layer and thesecondary coating layer are simultaneously coated.

The curing unit 40 includes one or a plurality of UV lamps 40 a, andforms the optical fiber 5 by curing the coating layer of the opticalfiber intermediary body 4. The curing unit 40, for example, includes aplurality of pairs of UV lamps 40 a which are disposed by interposing aspace therebetween through which the optical fiber intermediary body 4passes

As the position sensor 80, for example, a laser-type position sensor canbe employed. The position sensor 80 can detect a position of the bareoptical fiber 3. The position sensor 80 can measure a flotation amountof the bare optical fiber 3 at the second direction changer 20B based onthe positional information of the bare optical fiber 3.

The position sensor 80 outputs a detection signal to the control unit 90based on the information regarding the detected position of the bareoptical fiber 3.

Although it is not shown, the position sensor for the first directionchanger 20A can be disposed at a position between the first directionchanger 20A and the second direction changer 20B.

The position sensor can measure a flotation amount of the bare opticalfiber 3 at the second direction changer 20A based on the positionalinformation of the bare optical fiber 3.

The position sensor also outputs a detection signal to the control unit90 based on the information regarding the detected position of the bareoptical fiber 3.

The control unit 90 can control the Reynolds number (Re number) at eachof the direction changers 20A and 20B by adjusting the introduced flowvolume of the fluid flowed to each of the direction changers 20A and 20Bbased on the detection signal. The control unit 90 can control theintroduced flow volume of the fluid by, for example, adjusting anopening degree of an on-off valve provided on an introduction pathintroducing the fluid to the direction changers 20A and 20B.

The optical fiber 5 changes the direction thereof by a pulley 50 and istaken up by a take-up unit 60 and is wound by winding means 70.

The take-up unit 60, for example, is a take-up capstan, and determines afiber drawing speed. The fiber drawing speed, for example, is greaterthan or equal to 1500 m/min.

The winding means 70 is a winding bobbin which winds the optical fiber5.

An outer diameter of the optical fiber preform 2, for example, isgreater than or equal to 100 mm, and the length of the optical fiber 5prepared from one optical fiber perform 2, and for example, is a fewthousand km.

First, the direction will be defined. As shown in FIG. 1, a surfaceincluding a linear path line (a first path L1) of the bare optical fiber3 before being subjected to direction change by the direction changer20A and a linear path line (a second path L2) of the bare optical fiber3 after being subjected to the direction change of 90° by the directionchanger 20A is referred to as “P1”. An X direction is a direction alongthe second path L2 in the surface P1, and a Y direction is a directionperpendicular to the surface P1.

The optical fiber preform 2 is in a state of being suspended in thevertically downward direction, and the direction of the bare opticalfiber 3 which is drawn out from the optical fiber preform 2 is toward avertically lower portion. For this reason, in the disposition of thefirst direction changer 20A, accuracy in a disposing position of thedirection (the Y direction) perpendicular to the surface P1 includingthe first path L1 along a vertical direction and the second path L2along a horizontal direction is important.

The reason that accuracy in the positioning of the Y direction isimportant is because when the bare optical fiber 3 is in contact with aninside surface 21 c of the guide groove 21 of the direction changer 20,the strength of the bare optical fiber 3 decreases as shown in FIG. 2,and thus it is necessary to reliably separate the bare optical fiber 3from the inside surface 21 c.

In the manufacturing apparatus 1A, the direction of the bare opticalfiber 3 is changed to a third path L3 along the vertical direction bythe second direction changer 20B, and thus in the disposition of thesecond direction changer 20B, accuracy in the disposing position of thedirection (the Y direction) perpendicular to the surface P1 includingthe second path L2 and the third path L3 is required.

The resin coating is generally performed with respect to the verticallydownward bare optical fiber, and thus disposition accuracy in the Ydirection which is the direction perpendicular to a surface includingthe path L3 introduced to the coating unit 30 and the path L2 before thedirection change is important.

Furthermore, the direction of the bare optical fiber to be subjected tothe resin coating is not limited to the vertically downward direction.The direction may be a direction along the second path insofar as thecoating can be performed.

Hereinafter, a specific structure of the direction changer 20 will bedescribed.

A direction changer 201 shown in FIG. 3A, is a first example of thedirection changer 20 and is able to change the direction of the bareoptical fiber 3 by 90°. Therefore, the direction changer 201 can be usedas the direction changers 20A and 20B shown in FIG. 1.

The direction changer 201 is in the shape of one quarter circle in aplan view, and the guide groove 21 is formed over the entirecircumferential length in an outer circumferential surface 20 a. Thedirection changer 201 allows a central axis direction to be coincidentwith the Y direction, and disposes a radial direction D1 (refer to FIG.2) in a posture directed towards the direction along the surface P1(refer to FIG. 1). Here, a direction along the outer circumferentialsurface 20 a which is in the shape of an arc in a plan view is referredto as a circumferential direction.

A blowout port 22 for the fluid (air or the like) which floats the bareoptical fiber 3 wired along the guide groove 21 is formed in a lowerportion of the guide groove 21 along the guide groove 21. The blowoutport 22 is formed over the entire length of the guide groove 21.

As shown in FIG. 2, the direction changer 201 is configured to dischargethe fluid (for example, air) in a space (a fluid storing portion 25)ensured in the direction changer 201 into the guide groove 21 throughthe blowout port 22.

The direction changer 201, for example, can be configured to introducethe fluid to the fluid storing portion 25 from the outside, and todischarge the fluid into the guide groove 21 through the blowout port22.

It is preferable that the guide groove 21 is formed to be inclined withrespect to the radial direction D1 such that a distance between theinside surfaces 21 c and 21 c (a dimension in the Y direction) graduallyincreases towards an outer portion in the radial direction. It ispreferable that the two inside surfaces 21 c and 21 c have the sameinclination angle θ1 with respect to the radial direction D1.

In the direction changers 20A to 20C, the fluid (for example, air) inthe fluid storing portion 25 is discharged into the guide groove 21through the blowout port 22, and thus it is possible to float the bareoptical fiber 3. Specifically, a pressure difference between a deepportion 21 d and a shallow portion 21 e of the guide groove 21 increasesdue to the discharged air, and thus the bare optical fiber 3 is floatedby applying a force of the outer portion in the radial direction to thebare optical fiber 3.

In the above case, according to conditions, Karman vortex is generatedat an outer side in the radial direction to the bare optical fiber 3.When the Karman vortex is generated, pressure fluctuations occur and thebare optical fiber 3 is oscillated. Due to the oscillation, the bareoptical fiber 3 is possibly in contact with the inside surface 21 c.

The strength of the bare optical fiber 3 may decrease when contactingthe inside surface 21 c of the guide groove 21, and thus it is necessaryto reliably separate the bare optical fiber 3 from the inside surface 21c.

Therefore, the Karman vortex needs to be canceled or to be small enoughto reduce the vibration of the bare optical fiber 3.

In the direction changer 201, in order to reduce the Karman vortex, theRe number just before the fluid contacts the bare optical fiber 3 isdefined.

The Re number is an index indicating a laminar flow and turbulence of aflow, and when the Re number gets smaller, the flow becomes a laminarflow and less Karman vortex is generated. In contrast, when the Renumber gets larger, the flow becomes a laminar flow and more Karmanvortex is easily generated.

The Re number does not need to be constant in a circumferentialdirection of the direction changer 201, and as appropriate, the Renumber can be optimized in each of the sections located in differentpositions in the circumferential direction. Therefore, the oscillationof the bare optical fiber 3 can be reduced.

As to the Re number, it is desirable to optimize values at an inlet wireportion (a portion including a part in which the bare optical fiber 3moves into the guide groove) and an outlet wire portion (a portionincluding a part in which the bare optical fiber 3 moves out from guidegroove) of the bare optical fiber 3 in the direction changer. Therefore,it is possible to improve the stability of the bare optical fiber 3 whenit is floated.

In the direction changer 201 shown in FIG. 3A, the bare optical fiber 3moves into a first end 21 a of the guide groove 21 in the shape of onequarter circle and moves out from a second end 21 b, and thus issubjected to the direction change of 90°. An inlet wire portion 23 intowhich the bare optical fiber 3 moves is a portion including the firstend 21 a of the guide groove 21, and an outlet wire portion 24 fromwhich the bare optical fiber 3 moves out of is a portion including thesecond end 21 b of the guide groove 21.

FIG. 3B is a diagram in which the blowout port 22 is developed. As shownin this drawing, the blowout port 22 includes an intermediate portion 26having a constant width (a constant dimension in the Y direction) over apredetermined length range of the guide groove 21, a first end portion27 including the first end 22 a of the blowout port 22, and a second endportion 28 including the second end 22 b of the blowout port 22.

The first end portion 27 extends along the guide groove 21 while thewidth of the first end portion 27 is narrowed towards the first end 21 aof the guide groove 21 from one end of the intermediate portion 26. Thesecond end portion 28 extends along the guide groove 21 while the widthof the second end portion 28 is narrowed towards the second end 21 b ofthe guide groove 21 from the other end of the intermediate portion 26.

The first end 22 a of the blowout port 22 reaches the first end 21 a ofthe guide groove 21, and the second end 22 b reaches the second end 21b.

The first end portion 27 and the second end portion 28, for example, areportions in a circumferential direction range corresponding to 10° to30°.

In the direction changer 201 shown in FIG. 3A, the first end portion 27may be in a range in which a position of 0° is a starting end and aposition of 10° to 30° is a terminating end in a range of 90°. Inaddition, the second end portion 28 may be in a range in which aposition of 60° to 80° is the starting end and a position of 90° is theterminating end in the range of 90°. In this example, each of the firstend portion 27 and the second end portion 28 is in a circumferentialdirection range corresponding to 11.1% to 33.3% of the entire blowoutport 22.

In a direction changer 203 shown in FIG. 5A, a first end portion 37 maybe in a range in which a position of 0° is the starting end and aposition of 20° to 30° is the terminating end in a range of 180°. Inaddition, a second end portion 38 may be in a range in which a positionof 150° to 160° is the starting end and a position of 180° is theterminating end in the range of 180°. In this example, each of the firstend portion 37 and the second end portion 38 is in a circumferentialdirection range corresponding to 11.1% to 16.7% of the entire blowoutport 22.

It is difficult for the first end portion 27 and the second end portion28 to have a high flow rate in a range close to the first end 21 a andthe second end 21 b, and thus a portion including the first end 21 a andthe second end 21 b may be excluded.

In an example shown in FIG. 8, the first end portion 27 may be a portionexcluding a circumferential direction range (in FIG. 8, for example, arange of greater than or equal to 0° and less than 5°) including thefirst end 21 a. In addition, the second end portion 28 may be a portionexcluding a circumferential direction range (in FIG. 8, for example, arange of greater than 85° and less than or equal to 90°) including thesecond end 21 b.

That is, the first end portion 27 may be in a range in which a positionof 5° is the starting end and a position of 10° to 30° is theterminating end in a range of 90°. In addition, the second end portion28 may be in a range in which a position of 60° to 80° is the startingend and a position of 85° is the terminating end in the range of 90°.

In this example, each of the first end portion 27 and the second endportion 28 is in a circumferential direction range corresponding to 5.5%to 27.8% of the entire blowout port 22.

In an example shown in FIG. 9, the first end portion 37 may be a portionexcluding a circumferential direction range (in FIG. 9, for example,less than 10°) including a first end 31 a. In addition, the second endportion 38 may be a portion excluding a circumferential direction range(in FIG. 9, for example, a range of greater than 170° and less than orequal to 180° including a second end 31 b.

That is, the first end portion 37 may be in a range in which a positionof 10° is the starting end and a position of 20° to 30° is theterminating end in a range of 180°. In addition, the second end portion38 may be in a range in which a position of 150° to 160° is the startingend and a position of 170° is the terminating end in the range of 180°.

In this example, each of the first end portion 37 and the second endportion 38 is in a circumferential direction range corresponding to 5.5%to 11.1% of the entire blowout port 22.

It is not possible to comprehensively determine a difference between theminimum width of the first end portion 27 and the second end portion 28and the width of the intermediate portion 26 since the differencedepends on other designs, but the difference is at least on the order ofa few μm to a few dozen μm.

A difference between the minimum width of the first end portion 27 andthe second end portion 28, and the width of the intermediate portion 26,for example, is able to be 2 μm to 10 μm. By setting the difference tobe in the range described above, it is possible to ensure theblowing-out flow rate of the fluid in the first end portion 27 and thesecond end portion 28, and it is possible to increase a ratio of theblowing-out flow rate in the first end portion 27 and the second endportion 28 to the blowing-out flow rate in the intermediate portion 26.

It is preferable that the maximum width of the first end portion 27 andthe second end portion 28 and the width of the intermediate portion 26are equal to each other.

The minimum width of the first end portion 27 and the second end portion28 can be 70% to 98% with respect to the width of the intermediateportion 26. The minimum width of the first end portion 27 and the secondend portion 28 is preferably 80% to 95%, and is more preferably 85% to90%, with respect to the width of the intermediate portion 26.

By setting the ratio of the minimum width of the first end portion 27and the second end portion 28 to the width of the intermediate portion26 to be in the range described above, it is possible to ensure theblowing-out flow rate of the fluid in the first end portion 27 and thesecond end portion 28, and it is possible to increase a ratio of theblowing-out flow rate in the first end portion 27 and the second endportion 28 to the blowing-out flow rate in the intermediate portion 26.

Furthermore, in the first end portion 27, the second end portion 28, andthe intermediate portion 26 shown in FIG. 3B, both side edges arelinear, and when the width of the first end portion 27, the second endportion 28, and the intermediate portion 26 is narrowed towards thefirst end 21 a and the second end 21 b, both of the side edges may becurved.

In the direction changer 201 shown in FIGS. 3A, 3B, The width of thefirst end portion 27 and the second end portion 28 (for example, anaverage width or the minimum width) is narrowed, and thus the width ofthe blowout port 22 is narrowed in the inlet wire portion 23 and theoutlet wire portion 24 which are both end portions of the guide groove21.

For this reason, in the inlet wire portion 23 and the outlet wireportion 24, a pressure loss at the time of blowing out the fluid fromthe blowout port 22 increases compared to the other portion (in thisexample, a portion between the inlet wire portion 23 and the outlet wireportion 24, that is, a portion in a length range corresponding to theintermediate portion 26), and thus the blowing-out flow rate in theinlet wire portion 23 and the outlet wire portion 24 is faster than thelowest flow rate of the fluid in the other portion.

The blowing-out flow rate of the fluid in the inlet wire portion 23 andthe outlet wire portion 24 may be faster than an average flow rate (orthe highest flow rate) of the fluid in the intermediate portion 26.

In comparison to the flow rate of the fluid in the intermediate portion26, the flow rate of the fluid in the inlet wire portion 23 and theoutlet wire portion 24 is the average value or the highest value.

Since the blowing-out flow rate of the fluid increases at the inlet wireportion 23 and the outlet wire portion 24, the Re number increasescompared to the other portion (in this example, a portion including alength corresponding to the intermediate portion 26).

A direction changer 202 shown in FIG. 4 is a modification example of thedirection changer 201, and is in the shape of a three-quarter circle ina plan view. Hereinafter, the same reference numerals are applied toconfigurations identical to the configurations described above, and thedescription thereof will be omitted.

The direction changer 202 has a structure in which on an incoming lineside and an outgoing line side of a main body portion 29 a having thesame structure as that of the direction changer 201 shown in FIG. 3A,auxiliary portions 29 b and 29 c respectively having the same structureas that of the main body portion 29 a are continuously disposed.

The direction changer 202 has a basic function identical to that of thedirection changer 201 since the bare optical fiber 3 moves into theguide groove 21 of the main body portion 29 a from the inlet wireportion 23, and moves out through the outlet wire portion 24 after thedirection thereof is changed by 90° in the main body portion 29 a.

The direction changers 201 and 202 are able to change the direction ofthe bare optical fiber 3 by 90°, and thus are able to be used as thedirection changers 20A and 20B shown in FIG. 1.

The direction changer 203 shown in FIG. 5A is a second example of thedirection changer 20, and is able to change the direction of the bareoptical fiber 3 by 180°. The direction changer 203 is in the shape of asemicircle in a plan view, and a guide groove 31 is formed over theentire circumferential length in the outer circumferential surface 20 a.

A blowout port 32 of the fluid (air or the like) which floats the bareoptical fiber 3 is formed in a lower portion of the guide groove 31along the guide groove 31. The blowout port 32 is formed over the entirelength of the guide groove 31.

The direction changer 203 is configured to discharge the fluid in theguide groove 31 from the fluid storing portion 35 through the blowoutport 32.

In the direction changer 203, the bare optical fiber 3 moves into afirst end 31 a of the guide groove 31 which is in the shape of asemicircle, and is subjected to direction change of 180° by moving outfrom a second end 31 b. An inlet wire portion 33 is a portion includingthe first end 31 a of the guide groove 31, and an outlet wire portion 34is a portion including the second end 31 b of the guide groove 31.

The sectional shape of the guide groove 31 is the same as the sectionalshape of the guide groove 21 (refer to FIG. 2).

As shown in FIG. 5B, the blowout port 32 includes an intermediateportion 36 having a constant width (a constant dimension in the Ydirection) over a predetermined length range of the guide groove 31, afirst end portion 37 including the first end 32 a of the blowout port32, and a second end portion 38 including the second end 32 b of theblowout port 32.

The first end portion 37 extends along the guide groove 31 while thewidth of the first end portion 37 is narrowed towards the first end 31 aof the guide groove 31 from one end of the intermediate portion 36. Thesecond end portion 38 extends along the guide groove 31 while the widthof the second end portion 38 is narrowed towards the second end 31 b ofthe guide groove 31 from the other end of the intermediate portion 36.

The first end 32 a of the blowout port 32 reaches the first end 31 a ofthe guide groove 31, and the second end 32 b reaches the second end 31b.

The width of the first end portion 37 and the second end portion 38 (forexample, an average width or the minimum width) is narrowed, and thusthe width of the blowout port 32 is narrowed in the inlet wire portion33 and the outlet wire portion 34 which are both end portions of theguide groove 31.

For this reason, in the inlet wire portion 33 and the outlet wireportion 34, the blowing-out flow rate of the fluid from the blowout port32 is faster than the lowest flow rate of the fluid in the other portion(an intermediate portion 36).

The blowing-out flow rate of the fluid in the inlet wire portion 33 andthe outlet wire portion 34 may be faster than an average flow rate (orthe highest flow rate) of the fluid in the intermediate portion 36.

Since the blowing-out flow rate of the fluid increases at the inlet wireportion 33 and the outlet wire portion 34, the Re number increasescompared to the other portion (in this example, a portion including alength corresponding to the intermediate portion 36).

A direction changer 204 shown in FIG. 6 is a modification example of thedirection changer 203, and is in the shape of a three-quarter circle ina plan view.

The direction changer 204 has a structure in which on an incoming lineside and an outgoing line side of a main body portion 39 a having thesame structure as that of the direction changer 203 shown in FIG. 5A,auxiliary portions 39 b and 39 c respectively having the same sectionalstructure as that of the main body portion 39 a which are in the shapeof an eighth circle in a plan view are continuously disposed.

The direction changer 204 has a basic function identical to that of thedirection changer 203 since the bare optical fiber 3 moves into theguide groove 31 of the main body portion 39 a from the inlet wireportion 33, and moves out through the outlet wire portion 34 after thedirection thereof is changed by 180° in the main body portion 39 a.

Next, a first embodiment of a manufacturing method of an optical fiberof the present invention will be described by using a case where themanufacturing apparatus 1A is used as an example.

(Drawing Step)

In the drawing unit 10, the optical fiber preform 2 is heated and drawn,and thus the bare optical fiber 3 is formed.

(Direction Change of Direction Changer)

The bare optical fiber 3 which is drawn out to the vertically downwarddirection (the first path L1) from the optical fiber preform 2 isdirected towards a horizontal direction (the second path L2) due todirection change of 90° of the first direction changer 20A.

The bare optical fiber 3 is directed towards the vertically downwarddirection (the third path L3) due to direction change of 90° of thesecond direction changer 20B.

In the direction changers 20A and 20B, the fluid (for example, air) inthe fluid storing portion 25 is discharged into the guide groove 21through the blowout port 22, and thus it is possible to float the bareoptical fiber 3. Specifically, a pressure difference between the deepportion 21 d and the shallow portion 21 e of the guide groove 21increases due to the discharged air, and thus the bare optical fiber 3is floated by applying a force of the outer portion in the radialdirection to the bare optical fiber 3.

The position sensor 80 outputs a detection signal to the control unit 90based on the information regarding the detected position of the bareoptical fiber 3.

The control unit 90 controls the introduced flow volume of the fluidflowed to each of the direction changers 20A and 20B based on thedetected signal. The control unit 90 can control the introduced flowvolume of the fluid by, for example, adjusting an opening degree of anon-off valve provided on an introduction path introducing the fluid tothe direction changers 20A and 20B.

In particular, the control unit 90 controls the introduced flow volumeof the fluid to be decreased when the flotation amount of the bareoptical fiber 3 increases. As a result, the Re numbers at the directionchangers 20A and 20B are decreased. The control unit 90 controls theintroduced flow volume of the fluid to be increased when the flotationamount of the bare optical fiber 3 decreases. Therefore, the Re numberat each of the direction changers 20A and 20B increases.

As a control method, a feedback controller such as aproportional-integral-derivative (PID) controller is preferable.Therefore, the introduced flow volume of the fluid can be controlledwith satisfactory responsiveness

The position sensor for the first direction changer 20A can be disposedat a position between the first direction changer 20A and the seconddirection changer 20B. In this case, the flotation amount of the bareoptical fiber 3 at the first direction changer 20A is measured based onthe positional information of the bare optical fiber 3 obtained at thisposition sensor. Based on the measurement results thereof, the controlunit 90 can control the Re number of the first direction changer 20A.

In this case, the control of the Re number at the second directionchanger 20B is performed based on the positional information of the bareoptical fiber 3 obtained at the position sensor 80. In particular, theflotation amount of the bare optical fiber 3 at the second directionchangers 20B is measured based on the information obtained at theposition sensor 80. Based on the measurement results, the control unit90 controls the Re number of the second direction changer 20B.

(Coating Step)

In the coating unit 30, the coating material such as a urethaneacrylate-based resin is applied (coated) onto the outer circumference ofthe bare optical fiber 3 and becomes the coating layer, and thus theoptical fiber intermediary body 4 is obtained.

(Curing Step)

In the curing unit 40, the coating layer of the optical fiberintermediary body 4 is cured by irradiation of a UV lamp 40 a, and theoptical fiber 5 is formed.

The optical fiber 5 is wound by the winding means 70 through the pulley50 and the take-up unit 60.

As shown in FIG. 2, the flotation amount of the bare optical fiber 3inside the guide groove 21 depends on the flow rate of the fluid.

The inside surfaces 21 c, 21 c are inclined such that a width graduallyincreases towards an outer portion in the radial direction. Therefore,when the flotation amount of the bare optical fiber 3 increases, a gapbetween the bare optical fiber 3 and the inside surface 21 c increases,and the contact between the bare optical fiber 3 and the inside surface21 c hardly occurs.

However, practically, when the flotation amount of the bare opticalfiber 3 increases, the strength of the bare optical fiber 3 oftendecreases and the cause thereof is estimated as the contact between thebare optical fiber 3 and the inside surface 21 c.

The inventors of the present application found the followings afterconsideration of causes and solutions of the above phenomenon.

In the guide groove 21, by setting the Re number of the fluid flow justbefore the bare optical fiber 3 to be 1200-3500, floatation of the bareoptical fiber 3 can be stabilized.

When the Re number exceeds 3500, due to pressure fluctuations which islikely to be caused by an influence of Karman vortex of the fluid flowgenerated in the rear of the bare optical fiber 3, the flotation amountof the bare optical fiber 3 changes (temporal oscillation or fluctuationof the flotation amount of the bare optical fiber 3) occurs.

Due to the variation of the flotation amount, the bare optical fiber 3is in contact with the inside surfaces 21 c, 21 c with some frequencies,and the strength of the optical fiber 5 may decrease by the contact.

FIG. 7 is a diagram showing an example of fluctuation of a flotationposition.

Regarding the flotation amount, the manufacturing apparatus 1A of thebare optical fiber shown in FIG. 1 is used and positional data of thebare optical fiber 3 is obtained by the position sensor 80 disposed at aposition between the direction changer 20B and the coating unit 30 (thethird path L3).

With reference to FIG. 7, it is found that a flotation position of acomponent in an X-direction fluctuates much greater than a flotationposition of a component in a Y-direction as the time elapses. It appearsthat a position in the Y-direction is stable; however, the fluctuationof the flotation position is approximately ±10 μm. Usually, since a gapbetween the bare optical fiber 3 and an inside surface 21 c of the guidegroove 21 is a few tens μm, the fluctuation of the flotation position inthe Y-direction is not also a small fluctuation.

When the Re number is under 1200, the fluid flow becomes almost like alaminar flow. However, since a fluid-flow rate is slow, a sufficientflotation amount of the bare optical fiber 3, due to the variation ofthe drawing tension, the flotation position of the bare optical fiber 3is shifted in a depth direction of the guide groove 21 and the bareoptical fiber 3 contacts the surface 21 c. As a result, the strength ofthe bare optical fiber 3 is decreased.

In contrast, when the Re number of the fluid flow is 1200-3500, acertain amount of flotation amount of the bare optical fiber 3 issecured and the temporal stability of the flotation amount is obtained,and drawing can be performed without causing products to include aserious defect.

A Re number at the direction changer 20 can be calculated as shownbelow.Re number=density of gas to be used [kg/m³]×fluid-flow rate[m/sec]×representative length [m]/viscosity of gas to be used [Pa·s]

Regarding a representative length, since the inclination of the insidesurfaces 21 c, 21 c is very small, the inside surface 21 c, 21 c isassumed to be parallel each other, and a representative length betweenthe two plates.

Here, the Re number is introduced as an index to represent stability ofthe flotation amount. Therefore, the Re number does not need to bestrictly precise, and an upper-class index is used. In other words, whena distance between the two plates is d [m], the representative length isset 2 d [m].

In addition, with regard to the fluid-flow rate [m/sec], a measurementposition is at a bottom side of the guide groove 21 in a turningposition of the bare optical fiber 3. For example, a fluid-flow positionis follows: fluid-flow position=turning radius (center position of thebare optical fiber 3)−radius of the bare optical fiber 3. An outerdiameter of the bare optical fiber 3 is, for example, 125 μm.

A cross-section of the guide groove 21 at this position is calculated,and based on an introduced flow volume [m³/sec] of the fluid to adirection changer 20 as follows, fluid-flow rate [m/sec]=introduced flowvolume [m³/sec]/cross-section of fluid passage [m²], the fluid-flow rateis calculated.

Here, in the density of gas to be used and the viscosity of gas to beused, values at a temperature of used gas to be used (generally, anormal temperature and approximately 20° C.) are employed.

As a specific structure of the direction changer, for example,structures which are described in Japanese Patent No. 5571958 orJapanese Unexamined Patent Application, First Publication No. S62-003037can be used. The structure of the direction changer 20 is notparticularly limited to these two structures, and other structures maybe used.

For example, when a non-contact retaining mechanism described inJapanese Patent No. 5571958 is used, in the direction changer, adirection of the bare optical fiber 3 is changed by 90° at the turningradius of 62.5 mm. A width of the guide groove 21 (i.e., the width ofthe guide groove 21 at a position of an innermost periphery of the bareoptical fiber 3 in a floating state) is 145 μm. A diameter of the bareoptical fiber 3 is 125 μm. An introduced flow volume of the air is 100L/min with respect to the direction changer.

The turning radius is determined by a relation between a fluid-flow rateand drawing tension. Here, the turning radius is a radius when a certaindrawing tension is set under a structure or a manufacturing condition ofa specific direction changer.Fluid-flow position=62.5×10⁻³−62.5×10⁻⁶=0.0624375 mCross-section of fluid passage=2×π×Fluid-flow position×90/360×a groovewidth=1.42211×10⁻⁵ mFluid-flow rate=Introduced flow volume/Fluid-flowposition=100×10⁻³/60/cross-section of fluid passage≈117.2 m/secDensity of air (20° C.)=1.205 kg/m³Viscosity of air (20° C.)=1.822×10⁻⁵ Pa·sRepresentative length=a groove width×2=145×10⁻⁶×2=0.00029 mRe number≈2248

Since the Re number falls into a range of 1200 to 3500, the aboveconditions can be determined as the conditions in a stable state.

In addition, the Re number of the fluid flow does not need to beconstant at the entire circumferential direction (the entire blowoutport) of the direction changer 20, and as appropriate, the Re number canbe optimized in each of the sections located in different positions inthe circumferential direction.

For example, an inlet wire position and an outlet wire position of thebare optical fiber 3 to and from the direction changer 20 are on acontact interface of the bare optical fiber 3 and the fluid flow. Thecontact interface is an interface between a portion where the bareoptical fiber 3 contacts the fluid flow and a portion where the bareoptical fiber 3 does not contact the fluid flow.

Furthermore, it is necessary to correct the positional shift between atip end portion of the optical fiber at the manufacturing apparatus 1Aand the direction changer 20 (center shift) by the fluid flow in anyway. Therefore, in addition to a condition to obtain stability of thefloatation amount at a normal portion excluding an incoming lineposition and an outgoing line position, a condition for correct thepositional shift needs to be added.

For example, in FIG. 1, the optical fiber cannot be moved in a radialdirection, and thus the a tip end portion 2 a of a diameter reducedportion (neck-down) of the optical fiber preform 2 which is heated andmelted, the coating unit 30, the take-up unit 60, the pulley 50, and thewinding means 70 are able to act as a fixed end when the optical fiberis horizontally oscillated.

Regarding the direction changer 20, in order to correct a positionalshift of a path line of the bare optical fiber 3, it is desirable toincrease the flotation amount in the inlet wire portion 23 and theoutlet wire portion 24.

Therefore, as shown in FIG. 8, the Re number is adjusted to a largevalue as long as there is no influence of Karman vortex. In other words,the Re number is preferable to be at least in a range of 2500-3500.

As a result, the oscillation of the bare optical fiber 3 can bedecreased, and also the flotation stability in the inlet wire portion 23and the outlet wire portion 24 of the direction changer 20 can beobtained. In addition, a large allowable range of a positionalcorrection in the inlet wire portion 23 and the outlet wire portion 24can be secured. Accordingly, the decrease of the strength of the bareoptical fiber 3 due to the contact between the bare optical fiber 3 andthe inside surface 21 c, 21 c can be reduced.

In order to increase the flotation amounts at the inlet wire portion 23and the outlet wire portion 24, the Re number is set greater than the Renumber at the other portion (in this example, a portion between theinlet wire portion 23 and the outlet wire portion 24, that is, a portionin a length range corresponding to the intermediate portion 26).

In the direction changer 201 shown in FIGS. 3A and 3B, the width of thefirst end portion 27 and the second end portion 28 (for example, anaverage width or the minimum width) is narrowed, and thus the width ofthe blowout port 22 is narrowed in the inlet wire portion 23 and theoutlet wire portion 24 which are both end portions of the guide groove21.

For this reason, in the inlet wire portion 23 and the outlet wireportion 24, a pressure loss at the time of blowing out the fluid fromthe blowout port 22 increases compared to the other portion (in thisexample, a portion between the inlet wire portion 23 and the outlet wireportion 24, that is, a portion in a length range corresponding to theintermediate portion 26), and thus the blowing-out flow rate in theinlet wire portion 23 and the outlet wire portion 24 is faster than thelowest flow rate of the fluid in the other portion.

The blowing-out flow rate of the fluid in the inlet wire portion 23 andthe outlet wire portion 24 may be faster than an average flow rate (orthe highest flow rate) of the fluid in the intermediate portion 26.

Therefore, the Re number at the inlet wire portion 23 and the outletwire portion 24 can be greater than the Re number at the other portion(in this example, a portion including a length corresponding to theintermediate portion 26).

As described above, the flow rate of the fluid increases in the inletwire portion 23 and the outlet wire portion 24, and thus a pressuredifference between a deep portion 21 d (see FIG. 2) and a shallowportion 21 e of the guide groove 21 increases, a force in a direction(an outer portion in a radial direction) in which the bare optical fiber3 is floated increases due to Bernoulli effect. In addition, based onthe Navier-Stokes principle considering viscosity, an effect positioningthe bare optical fiber 3 closer to a center of the guide groove 21 (acenter in the Y-direction) increases. For this reason, a shift in a pathline position is corrected.

In addition, a flotation amount of the bare optical fiber 3 increases inthe inlet wire portion 23 and the outlet wire portion 24. Thus, a gapbetween an inside surface 21 c of the guide groove 21 and the bareoptical fiber 3 is widened, and an acceptable amount with respect to theshift in the path line position increases.

For this reason, it is possible to relax a requirement for accuracy in adisposing position of the direction changer 20. For example, it ispossible to set disposing position required accuracy to be on a μm-orderto 0.5 mm order (a few hundred μm order), and it is possible to relax arequirement for accuracy of at least a few hundred times.

Accordingly, a disposing operation of the direction changer 20 becomeseasy, and damage which is caused by bringing the bare optical fiber 3 incontact with the inside surface 21 c of the guide groove 21 isprevented, and thus it is possible to manufacture the optical fiber 5with a sufficient yield.

Further, it is possible to adjust the blowing-out flow rate of the fluidin the inlet wire portion 23, the outlet wire portion 24, and theintermediate portion 26. Thus it is possible to ensure the blowing-outflow rate of the fluid for floating the bare optical fiber 3 in theintermediate portion 26. In addition, it is possible to set a sufficientblowing-out flow rate of the fluid for adjusting the path line positionin the inlet wire portion 23 and the outlet wire portion 24 and foradjusting the flotation amount of the bare optical fiber 3. Accordingly,it is possible to reduce the operating cost without wasting the fluid.

Regarding an adjustment of an installing position of the directionchangers 20A and 20B with respect to the X-direction, the same accuracyas in the Y-direction is not necessary. It is because that regarding theX-direction, for example, a flotation position of the bare optical fiberis finely adjustable by adjusting the number in a range of 1200-3500.

Therefore, in the X-direction, if disposition accuracy is in a rangecapable of ensuring the stability of the flotation amount of the bareoptical fiber 3 by at least adjusting the blowing-out flow rate of thefluid, the disposition accuracy may be low compared to the dispositionaccuracy in the Y-direction. In other words, it is desirable that if itcan be avoided a state that the bare optical fiber 3 does not float as aresult of decreasing the Re number by reducing the blowing-out flow rateof the fluid in order to adjust a position in an X-direction.

FIG. 8 shows an Re number distribution in a circumferential direction ofthe direction changer 201 (refer to FIGS. 3A and 3B) which changes thedirection of the bare optical fiber 3 by 90°. FIG. 9 shows an Re numberdistribution in a circumferential direction of the direction changer 203(refer to FIGS. 5A and 5B) which changes the direction of the bareoptical fiber 3 by 180°. In the measurement, a wind gauge SAV-26Amanufactured by Kansai Tech Co., Ltd. is used, but the wind gauge is notparticularly limited. The amount of the fluid (air) introduced to thedirection changer 201 is suitably adjusted such that the amount does notexceed a measurement upper limit of the wind gauge. Here, based on themeasured wind-speed distribution, the distribution is converted to awind speed at a position where the Re number is calculated and regardedas the actual introduced flow volume of the fluid, and converted to anRe-number distribution.

As shown in FIG. 8, in the direction changer 201 (refer to FIGS. 3A and3B) which changes the direction of the bare optical fiber 3 by 90°, themeasurement is performed at a plurality of positions in thecircumferential direction every 5°. In this example, a position of 0° isan incoming line position, and a position of 90° is an outgoing lineposition.

As shown in this drawing, the Re number is maximized in a position closeto the incoming line position and the outgoing line position (a positionof 10° and 80°), and the Re number is minimized in a position separatedfrom the incoming line position and the outgoing line position (aposition of 35° and 55°.

The Re number in a position of 10° is the highest value of theblowing-out Re number of the fluid in the inlet wire portion 23 of thedirection changer 201 (refer to FIGS. 3A and 3B). The wind speed in aposition of 80° is the highest value of the blowing-out Re number of thefluid in the outlet wire portion 24 of the direction changer 201.

The Re number in a position of 35° and 55° is the lowest value of theblowing-out Re number of the fluid in the intermediate portion 26 of thedirection changer 201.

The blowing-out Re number (the highest value) in the inlet wire portion23 and the outlet wire portion 24 is approximately 1.8 times the lowestvalue of the blowing-out Re number in the intermediate portion 26.

As shown in FIG. 9, in the direction changer 203 (refer to FIGS. 5A and5B) which changes the direction of the bare optical fiber 3 by 180°, themeasurement is performed at a plurality of positions in thecircumferential direction every 10°. In this example, a position of 0°is an incoming line position, and a position of 180° is an outgoing lineposition.

As shown in this drawing, the Re number is maximized in a position closeto the incoming line position and the outgoing line position (a positionof 20° and 160°), and the Re number is minimized in a position separatedfrom the incoming line position and the outgoing line position (aposition of 70°).

The Re number in a position of 20° is the highest value of theblowing-out flow rate of the fluid in the inlet wire portion 33 of thedirection changer 203 (refer to FIGS. 5A and 5B). The Re number in aposition of 160° is the highest value of the blowing-out flow rate ofthe fluid in the outlet wire portion 34 of the direction changer 203.

The Re number in a position of 70° is the lowest value of theblowing-out Re number of the fluid in the intermediate portion 36 of thedirection changer 203.

The blowing-out Re number (the highest value) in the inlet wire portion33 and the outlet wire portion 34 is approximately 1.8 times the lowestvalue of the blowing-out Re number in the intermediate portion 36.

Hereinafter, practically, a concrete method setting the Re numbers sothat the numbers are different in each of the plurality of areas in acircumferential direction is described.

1. Adjusting Re Number by Adjusting Width of Blowout Port 22

In the direction changer 201 shown in FIGS. 3A and 3B, the width of thefirst end portion 27 and the second end portion 28 (for example, anaverage width or the minimum width) is narrowed, and thus the width ofthe blowout port 22 is narrowed in the inlet wire portion 23 and theoutlet wire portion 24 which are both end portions of the guide groove21.

For this reason, in the inlet wire portion 23 and the outlet wireportion 24, a pressure loss at the time of blowing out the fluid fromthe blowout port 22 increases compared to the other portion (in thisexample, a portion between the inlet wire portion 23 and the outlet wireportion 24, that is, a portion in a length range corresponding to theintermediate portion 26), and thus the blowing-out flow rate in theinlet wire portion 23 and the outlet wire portion 24 is faster than thelowest flow rate of the fluid in the other portion.

As shown in FIG. 8, at the inlet wire portion 23 and the outlet wireportion 24, the blowing-out flow rate of the fluid becomes faster, theRe numbers increase compared to the another portion (in this example, aportion having a length range corresponding to the intermediate portion26).

2. Adjusting Re Number by Providing Multiple Inner Spaces

The direction changer 205 shown in FIG. 10 is a third example of thedirection changer 20, and is able to change the direction of the bareoptical fiber 3 by 180°. The direction changer 205 is in the shape of asemicircle in a plan view, and is configured to discharge the fluid inthe guide groove 31 from a fluid storing portion 45 through a blowoutport 42.

The shape of the blowout port 42 is not particularly limited, and forexample, the width may be constant over the length direction of theguide groove 31.

The fluid storing portion 45 is partitioned into a first fluid storingportion 45A (a first space) and a second fluid storing portion 45B (asecond space) by the partition wall 41.

The first fluid storing portion 45A is in communication with a first endportion 47 and a second end portion 48 of the blowout port 42, and thesecond fluid storing portion 45B is in communication with anintermediate portion 46 of the blowout port 42.

A first supply port 43A which supplies the fluid to the first fluidstoring portion 45A and a second supply port 43B which supplies thefluid to the second fluid storing portion 45B are formed on a sidesurface of the direction changer 205.

In the direction changer 205, a flow volume of the fluid supplied to thefluid storing portions 45A and 45B through the supply ports 43A and 43Bis adjusted, and thus it is possible to set inner pressures of the fluidstoring portions 45A and 45B to be independent from each other. For thisreason, it is possible to set the blowing-out flow rate of the fluid inthe first end portion 47 and the second end portion 48 and theblowing-out flow rate of the fluid in the intermediate portion 46 to beindependent from each other.

For this reason, it is possible to set the blowing-out flow rate of thefluid in the inlet wire portion 33 and the outlet wire portion 34 to befaster than the lowest blowing-out flow rate of the fluid in the otherportion in circumferential direction (the intermediate portion 46).

Since the blowing out flow rate of the fluid becomes fast at the inletwire portion 33 and the outlet wire portion 34, an Re number thereofbecomes faster than an Re number at the other portion (the intermediateportion 46) in the circumferential direction.

A direction changer 206 shown in FIG. 11 is a fourth example of thedirection changer 20, and is able to change the direction of the bareoptical fiber 3 by 180°. The direction changer 206 is in the shape of asemicircle in a plan view and is configured to discharge the fluid inthe guide groove 31 from a fluid storing portion 55 through a blowoutport 52.

The fluid storing portion 55 is partitioned into first to third fluidstoring portions 55A to 55C by partition walls 51A and 51B.

The first fluid storing portion 55A (a first space) is in communicationwith a first end portion 57 of the blowout port 52, the second fluidstoring portion 55B (a second space) is in communication with anintermediate portion 56 of the blowout port 52, and the third fluidstoring portion 55C (a third space) is in communication with a secondend portion 58 of the blowout port 52.

A first supply port 53A which supplies the fluid to the first fluidstoring portion 55A, a second supply port 53B which supplies the fluidto the second fluid storing portion 55B, and a third supply port 53Cwhich supplies the fluid to the third fluid storing portion 55C areformed on a side surface of the direction changer 206.

In the direction changer 206, the flow volume of the fluid supplied tothe fluid storing portions 55A to 55C through the supply ports 53A to53C is adjusted, and thus it is possible to set the blowing-out flowrate of the fluid in the first end portion 57 and the second end portion58 and the blowing-out flow rate of the fluid in the intermediateportion 56 to be independent from each other.

For this reason, it is possible to set the blowing-out flow rate of thefluid in the inlet wire portion 33 and the outlet wire portion 34 to befaster than the lowest blowing-out flow rate of the fluid in the otherportion in the circumferential direction (the intermediate portion 56).

Since the blowing out flow rate of the fluid becomes fast at the inletwire portion 33 and the outlet wire portion 34, an Re number thereofbecomes faster than an Re number at the other portion (the intermediateportion 56) in the circumferential direction.

3. Adjusting Re Number by Providing Narrow Portion

A direction changer 207 shown in FIG. 12 is a fifth example of thedirection changer 20 and is able to change the direction of the bareoptical fiber 3 by 90°.

The direction changer 207 is in the shape of one quarter circle in aplan view and is configured to discharge the fluid in a guide groove 61from a fluid storing portion 65 through a blowout port 62.

As shown in FIG. 13A, narrow portions 69 and 69 in which the width of aflow path is narrowed by the fluid storing portion 65 are formed betweenthe fluid storing portion 65 and the guide groove 61 in acircumferential direction range in which communication occurs with afirst end portion 67 and a second end portion 68 of the blowout port 62.

As shown in FIG. 13B, the narrow portion 69 is not formed in acircumferential direction range in which communication occurs with anintermediate portion 66 of the blowout port 62.

For this reason, in the circumferential direction range corresponding tothe first end portion 67 and the second end portion 68, a pressure lossat the time of blowing out the fluid increases compared to thecircumferential direction range corresponding to the intermediateportion 66.

In the direction changer 207, the narrow portions 69 and 69 are formedin the range corresponding to the first end portion 67 and the secondend portion 68, and thus in the inlet wire portion 23 and the outletwire portion 24, the blowing-out flow rate of the fluid from the blowoutport 62 is faster than the lowest flow rate of the fluid in the otherportion (the intermediate portion 66).

Since the blowing out flow rate of the fluid becomes fast at the inletwire portion 23 and the outlet wire portion 24, an Re number thereofbecomes faster than an Re number at the other portion (the intermediateportion 26) in the circumferential direction.

FIG. 14 is a schematic view showing a schematic configuration of amanufacturing apparatus 1B which is a second embodiment of themanufacturing apparatus of an optical fiber according to the presentinvention.

The manufacturing apparatus 1B is different from the manufacturingapparatus 1A shown in FIG. 1 in that the manufacturing apparatus 1Bincludes three direction changers 20 (20A, 20C, and 20D). Hereinafter,the second embodiment of the manufacturing method of an optical fiber ofthe present invention will be described.

In the manufacturing apparatus 1B, the bare optical fiber 3 which isdrawn out from the optical fiber preform 2 to the vertically downwarddirection (the first path L1) is directed towards the horizontaldirection (the second path L2) due to direction change of 90° of thefirst direction changer 20A.

The bare optical fiber 3 is directed towards a direction opposite to thesecond path L2 (a third path L4) due to direction change of 180° of thesecond direction changer 20C and is directed towards the verticallydownward direction (a fourth path L5) due to direction change of 90° ofa third direction changer 20D.

The bare optical fiber 3 is subjected to the resin coating in thecoating unit 30 and the coating layer is cured by the curing unit 40,and thus the optical fiber 5 is obtained.

The optical fiber 5 is wound by the winding means 70 through the pulley50 and the take-up unit 60.

EXAMPLES Example 1

The manufacturing apparatus 1A shown in FIG. 1 was prepared.

As the direction changers 20A and 20B, the direction changer 201 shownin FIGS. 3A and 3B was used. A width of the guide groove 21 is uniformin a depth direction.

A turning radius was approximately 62.5 mm. The width of the guidegroove 21 (i.e., the width of the guide groove 21 at a position of aninnermost periphery of the bare optical fiber 3 in a floating state) is145 μm.

Re numbers (calculated values) of the direction changers 20A and 20Bwere approximately 2248.

The fluid introduced to the direction changers 20A and 20B was air, andthe temperature thereof was room temperature (approximately 24° C.).

An introduced flow volume of the air was 100 liters/minute with respectto each of the direction changers 20A and 20B.

The first direction changer 20A was disposed in a position in which thetemperature of the bare optical fiber 3 was approximately 1000° C.

When the direction changers 20A and 20B were disposed, a centering(position adjustment of the path line) was performed in an accuracy of apm-order by a centering device using a laser.

The optical fiber preform 2 was drawn by the drawing unit 10, and thusthe bare optical fiber 3 (an outer diameter of 125 μm) was obtained. Asa drawing speed and drawing tension, general conditions (a drawing speedof 30 m/second, and drawing tension of approximately 150 gf) wereadopted.

The bare optical fiber 3 which was drawn out from the optical fiberpreform 2 to the vertically downward direction (the first path L1) wassubjected to direction change to the horizontal direction (the secondpath L2) by the first direction changer 20A, and then was subjected tothe direction change to the vertically downward direction (the thirdpath L3) by the second direction changer 20B. The length of the secondpath L2 was approximately 1 m.

In the coating unit 30, the bare optical fiber 3 was coated with anultraviolet curing resin and irradiated with ultraviolet rays by the UVlamp 40 a in the curing unit 40, the coating layer was cured, and thusthe optical fiber 5 was obtained.

The optical fiber 5 was wound by the winding means 70 through the pulley50 and the take-up unit 60.

While manufacturing the optical fiber 5 from the optical fiber preform2, an air supply to the direction changers 20A and 20B is reduced andthe Re number (a calculated value) is adjusted to be 1200.

In addition, while manufacturing the optical fiber 5 from the opticalfiber preform 2, an air supply to the direction changers 20A and 20B isincreased and the Re number (a calculated value) is adjusted to be 3500.

In the manufacturing method, in both conditions, it was confirmed thatthe bare optical fiber 3 was not damaged by the direction changers 20Aand 20B, and the optical fiber 5 was able to be manufactured with asufficient yield.

Example 2

In the manufacturing apparatus 1A shown in FIG. 1, an introduced flowvolume of the fluid to the direction changers 20A and 20B was controlledby using the position sensor 80 and the control unit 90.

In other words, by the position sensor 80, the positional information ofthe bare optical fiber 3 (flotation amount in the second directionchanger 20B) is obtained to output a detected signal to the control unit90, and an introduced flow volume of the fluid to the direction changers20A, 20B is controlled by the control unit 90.

As a control method, a PID controller is employed. Other conditions arein line with Example 1 to manufacture the optical fiber 5.

While manufacturing the optical fiber 5, variation of a linear speed is±50 m/min at maximum, and variation of the drawing tension is ±25 gf atmaximum.

However, in the direction changers 20A, 20B, since the flow volume ofthe air was controlled in a range of the Re number of 1200-3500, theflotation amount of the bare optical fiber 3 was ±0.05 mm and stable.

In the manufacturing method, it was confirmed that the bare opticalfiber 3 was not damaged by the direction changers 20A and 20B, and theoptical fiber 5 was able to be manufactured with a sufficient yield.

Example 3

In the manufacturing apparatus 1A shown in FIG. 1, as the directionchangers 20A and 20B, a direction changer 201 having an Re-numberprofile shown in FIG. 8 is used. The width of the intermediate portion26 in the blowout port 22 is 50 μm, and the minimum width of the firstend portion 27 and the second end portion 28 is 45 μm.

As shown in FIG. 2, an inclination angle θ1 of the inside surface 21 cof the guide groove 21 with respect to the radial direction D1 was 0.5°.A turning radius was approximately 62.5 mm.

The Re number at a portion excluding the inlet wire portion 23 and theoutlet wire portion 24 (i.e., a portion corresponding to theintermediate portion 26) was 2200, and the Re number at the inlet wireportion 23 and the outlet wire portion 24 was 2500. The inlet wireportion 23 and the outlet wire portion 24 are portions in acircumferential direction corresponding to a range having an angle of30° from each end.

When the direction changers 20A and 20B were disposed, a thread havingan outer diameter of 0.5 mm was used instead of the bare optical fiber3, and was centered by visual contact (position adjustment of the pathline).

In the manufacturing method, it was confirmed that the bare opticalfiber 3 was not damaged by the direction changers 20A and 20B, and theoptical fiber 5 was able to be manufactured with a sufficient yield.

Example 4

The optical fiber 5 was manufactured by using the manufacturingapparatus 1B shown in FIG. 14 as follows.

As the first direction changer and the third direction changer 20A and20D, the direction changer 201 having the same specification as thatused in Example 1 was used.

As the second direction changer 20C, the direction changer 205 shown inFIG. 10 was used.

An Re number at the inlet wire portion 33 and the outlet wire portion 34is set to 3000. An Re number at an area corresponding to theintermediate portion 46 is set to 1800.

When the direction changers 20A and 20B were disposed, a thread havingan outer diameter of 0.5 mm was used instead of the bare optical fiber3, and was centered by visual contact (position adjustment of the pathline).

In the manufacturing method, it was confirmed that the bare opticalfiber 3 was not damaged by the direction changers 20A, 20C, and 20D, andthe optical fiber 5 was able to be manufactured with a sufficient yield.

Example 5

In the manufacturing apparatus 1A shown in FIG. 1, the optical fiber 5was manufactured by the same method as that in Example 1 except that thedirection changer 207 shown in FIGS. 12 to 13B was used in the directionchangers 20A and 20B instead of the direction changer 201

An Re number at the inlet wire portion 23 and the outlet wire portion 24is set to 3500. An Re number at an area corresponding to theintermediate portion 26 is set to 3000.

When the direction changers 20A and 20B were disposed, a thread havingan outer diameter of 0.5 mm was used instead of the bare optical fiber3, and was centered by visual contact (position adjustment of the pathline).

In the manufacturing method, it was confirmed that the bare opticalfiber 3 was not damaged by the direction changers 20A and 20B, and theoptical fiber 5 was able to be manufactured with a sufficient yield.

Comparative Example 1

The optical fiber 5 was manufactured by using the manufacturingapparatus 1A shown in FIG. 1 by the same method as that in Example 1except that the Re number was 4000.

When manufacturing the optical fiber 5, the fluctuation of a flotationposition of the bare optical fiber 3 as in FIG. 7 was shown.

In the manufacturing method, breaking which was considered to be causedby bringing the bare optical fiber 3 in contact with the inside surfaceof the guide groove occurred. Thus, the manufacturing yield was notsufficient.

Comparative Example 2

The optical fiber 5 was manufactured by using the manufacturingapparatus 1A shown in FIG. 1 by the same method as that in Example 1except that the Re number was 1000.

When manufacturing the optical fiber 5, the fluctuation of a flotationposition of the bare optical fiber 3 as in FIG. 7 was shown.

In the manufacturing method, breaking which was considered to be causedby bringing the bare optical fiber 3 in contact with the inside surfaceof the guide groove occurred. Thus, the manufacturing yield was notsufficient.

While preferred embodiments of the invention have been described andillustrated above, it should be understood that these are exemplary ofthe invention and are not to be considered as limiting. Additions,omissions, substitutions, and other modifications can be made withoutdeparting from the spirit or scope of the present invention.Accordingly, the invention is not to be considered as being limited bythe foregoing description, and is only limited by the scope of theappended claims.

What is claimed is:
 1. An apparatus for manufacturing an optical fiber, comprising: a drawing portion configured to draw an optical fiber perform and form a bare optical fiber; a coating portion configured to dispose a coating layer formed of a resin on an outer circumference of the bare optical fiber; and a curing portion configured to cure the coating layer, wherein: a direction changer which changes a direction of the bare optical fiber is disposed in any position from the drawing portion to the coating portion; the direction changer includes a guide groove which guides the bare optical fiber; a blowout port of a fluid which floats the bare optical fiber wired along the guide groove is formed along the guide groove in the guide groove; and the blowout port is configured such that a Reynolds number in an inlet wire portion of the bare optical fiber entering the guide groove and a Reynolds number of an outlet wire portion of the bare optical fiber outputting from the guide groove is greater than a Reynolds number in an intermediate portion between the inlet wire portion and the outlet wire portion.
 2. The apparatus for manufacturing an optical fiber according to claim 1, wherein the Reynolds number of the fluid in the inlet wire portion and the outlet wire portion is set to be greater than the Reynolds number of the fluid in the intermediate portion such that a width of the blowout ports in the inlet wire portion and the outlet wire portion is set to be smaller than the blowout port in the intermediate portion.
 3. The apparatus for manufacturing an optical fiber according to claim 1, wherein an inner space portion which transports the fluid to the blowout port is ensured inside the direction changer, and the inner space portion includes a first space portion which is in communication with the blowout port of the inlet wire portion and the outlet wire portion, and a second space portion which is in communication with the blowout port of the intermediate portion.
 4. The apparatus for manufacturing an optical fiber according to claim 1, wherein an inner space portion which transports the fluid to the blowout port is ensured inside the direction changer, and the inner space portion includes a first space portion which is in communication with the blowout port of the inlet wire portion, a second space portion which is in communication with the blowout port of the intermediate portion, and a third space portion which is in communication with the blowout port of the outlet wire portion.
 5. The apparatus for manufacturing an optical fiber according to claim 1, wherein a narrow portion which is in communication with the blowout ports in the inlet wire portion and the outlet wire portion is formed inside the direction changer, and a pressure loss at the time of blowing out the fluid in the inlet wire portion and the outlet wire portion is greater than the pressure loss in the intermediate portion, thereby, the Reynolds number of the fluid in the inlet wire portion and the outlet wire portion is set to be greater than the Reynolds number of the fluid in the intermediate portion.
 6. The apparatus of manufacturing an optical fiber according to claim 1, wherein each of the inlet wire portion and the outlet wire portion is provided in a circumferential direction range corresponding to 11.1% to 33.3% of the entire blowout port. 